| HS Code | 815586 |
| Base Polymer | High Density Polyethylene (HDPE) |
| Filler | Glass Fiber |
| Filler Content | 40% |
| Uv Stabilization | Yes |
| Density | 1.23 g/cm³ |
| Melt Flow Index | 2.5 g/10 min at 190°C/2.16 kg |
| Tensile Strength | 60 MPa |
| Elongation At Break | 3% |
| Flexural Modulus | 4500 MPa |
| Izod Notched Impact Strength | 80 J/m |
| Heat Deflection Temperature | 135°C at 1.82 MPa |
| Vicat Softening Point | 130°C |
| Rockwell Hardness | R95 |
| Water Absorption | 0.02% |
| Molding Shrinkage | 0.3% |
| Processing Method | Injection Molding |
As an accredited Aclo Compounders HDPE HD0234G40UVL factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Aclo Compounders HDPE HD0234G40UVL is supplied in 25 kg moisture-resistant bags, palletized and shrink-wrapped for safe industrial storage and transport. |
| Container Loading (20′ FCL) | Aclo Compounders HDPE HD0234G40UVL loaded in 25 kg bags, palletized, shrink-wrapped, and secured inside a clean, dry 20-foot FCL container. |
| Shipping | Aclo Compounders HDPE HD0234G40UVL is typically shipped as a non-hazardous thermoplastic compound in 25 kg polyethylene bags, palletized, stretch-wrapped, and labeled with batch details. Transport in clean, dry trucks/containers, avoiding heat, moisture, sunlight, and incompatible materials. Follow SDS, packaging, and local transport regulations. |
| Storage | Store Aclo Compounders HDPE HD0234G40UVL indoors in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags or containers sealed and palletized off the floor. Prevent moisture, contamination, and prolonged UV exposure. Protect from physical damage. Follow local regulations, manufacturer’s SDS, and first-in, first-out stock rotation. Maintain good housekeeping. Store away from foodstuffs. |
| Shelf Life | Typically 24 months from manufacture when stored unopened in original packaging under cool, dry, ventilated conditions, away from direct sunlight. |
For structural injection-molded brackets and equipment housings where outdoor exposure introduces freeze-thaw humidity cycles, Aclo Compounders HDPE HD0234G40UVL is processed neat at the 40 wt% glass-fiber loading indicated by the grade designation; when a molder blends the grade with unfilled HDPE to reduce anisotropy, the letdown should not exceed 25 wt% unless tensile modulus is revalidated against ISO 527-2:2012. Grade-specific datasheet values should be verified against the supplier certificate of analysis because published data for this exact compound configuration is limited. General incoming inspection verifies filler content by ash content under ISO 3451-1:2019 and density under ISO 1183-1:2019. Sector compliance documentation normally references ISO 527-2:2012 for tensile properties, ISO 178:2019 for flexural modulus, ISO 179-1/1eA for Charpy notched impact, and ISO 4892-2:2013 for UV weathering; conflict minerals and restricted substances are managed through REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU. The production route is high-pressure injection molding on machines with clamp force from 1,800 kN to 8,000 kN, using a general-purpose screw with L/D between 18:1 and 22:1 and a non-return ring hardened to HRC 55 or higher because the glass fibers generate measurable screw and barrel wear. Barrel temperatures are held at 220 °C to 250 °C, mold surface temperature at 35 °C to 60 °C, and back pressure at 0.4 MPa to 0.8 MPa; exceeding 260 °C melt temperature triggers low-molecular-weight species formation and surface splay. Pre-drying at 80 °C for 2 h is required when ambient relative humidity exceeds 60 %. End products include pump mounting plates, ventilation louvre frames, chemical dosing cabinet brackets, and agricultural sensor enclosures.
Electrical and electronic enclosure applications expose glass-fiber-reinforced HDPE to a specific failure mode: weld-line fracture at the knit point between flow fronts. For HD0234G40UVL, the recommended formulation practice is to run the compound as supplied without additional impact modifier unless a low-temperature requirement below -20 °C is specified; if such a requirement exists, blending with an ethylene-octene toughener at 5 wt% to 10 wt% may be evaluated, but published data for this specific configuration is limited and full ISO 179-1/1eA testing at -30 °C is required. The downstream process is multi-cavity injection molding with valve-gated hot runners or direct edge gates having a minimum diameter of 1.5 mm; smaller gates produce excessive fiber breakage and a reduction in knit-line tensile strength exceeding 30 % relative to solid-section values. The melt temperature window is held narrow, typically 225 °C to 245 °C with a target of 235 °C, because below 225 °C the viscosity rise increases fiber attrition at the gate, and above 245 °C degradation by-products deposit on mold vents. Mold steel should be hardened to HRC 50 minimum, and vent depth must not exceed 0.02 mm to prevent glass-filled flash while permitting gas escape. Compliance in this segment is assessed under IEC 60695-11-10 for HB classification, and for installations near energized parts, IEC 60695-2-11 glow-wire testing at 650 °C is performed, although the grade itself is not inherently flame-retardant. End product categories include terminal junction boxes, outdoor lighting driver housings, cable splice enclosures, and industrial control panel covers.
Compression molding of pallet deck skins and dunnage trays uses HD0234G40UVL as the 100% polymer matrix; the process permits regrind incorporation up to 15 wt% for non-load-bearing dunnage and 5 wt% for load-bearing deck skins, with the addition ratio measured by batch weighment before dry blending. Because compression molding operates at lower shear than injection molding, fiber length retention is higher, and the critical process variable is press closing speed rather than injection velocity. The material is preheated to 190 °C to 210 °C in an infrared oven, transferred to a matched-metal mold, and compression molded at 8 MPa to 15 MPa hydraulic pressure for 4 min to 10 min depending on part thickness; release from the tool is assisted by a non-silicone mold release because silicone contamination weakens weld adhesion in subsequent ultrasonic joining. Industry compliance is anchored to ISO 8611-1:2021 for pallet load ratings and ISO 8611-2:2022 for racking performance, with fire certification typically requiring the end-user to apply an independent flame-retardant topcoat, since HDPE is not intrinsically fire-rated. End products include hygienic logistics pallets, meat and poultry transport trays, reusable dunnage boards, and collapsible sleeve-pack bases.
HD0234G40UVL is run on high-torque single-screw extruders with grooved feed sections and a barrier screw; screw L/D for this profile extrusion route is maintained between 30:1 and 36:1, and the screw and barrel must be nitrided or bimetallic because the glass fiber content accelerates wear at the compression zone. The extrusion temperature profile from feed to die is set at 170 °C, 190 °C, 210 °C, 225 °C, 235 °C, and die temperature 240 °C; melt pressure at the breaker plate is expected to remain below 25 MPa to avoid excessive shear heating. Formulation practice for outdoor cable tray channel is neat 100% compound with no additional UV masterbatch, because the grade designation includes UV-light stabilization; if post-industrial scrap is re-extruded, the top-up addition of a hindered-amine light stabilizer masterbatch at 1 wt% to 2 wt% may be required after 3 recycling loops, as determined by ISO 4892-2:2013 cycle 1 exposure. Sector compliance invokes IEC 61537:2023 for cable tray systems, ISO 178:2019 for flexural modulus, and ISO 4892-2:2013 for Xenon-arc weathering; load deflection under the relevant span is checked using ASTM D648-18 at 1.82 MPa. End products include UV-stabilized cable tray side rails, runway covers, solar farm wire-management profiles, and ventilation louvre blades.
Chemical processing equipment manufacturers replacing powder-coated steel with glass-filled HDPE use HD0234G40UVL for its resistance to acids, alkalis, and chlorinated solutions at ambient and moderate elevated temperatures. The material is injection molded or machined from compression-molded sheet; machining does not permit post-mold stress relief, so a final annealing step at 100 °C for 1 h per 25 mm of wall thickness is applied to reduce residual stress before chemical exposure. The formulation addition ratio in this segment is near 100% virgin compound; if blended with conductive carbon black for electrostatic dissipation, the addition is limited to 3 wt% to 5 wt%, but this alters weld integrity and requires revalidation of chemical resistance under ISO 175:2010 and ASTM D543-21. Downstream production includes injection molding machines with clamp force from 2,500 kN to 8,500 kN and tooling with full-length ejector sleeves to minimize warpage during ejection; melt temperature is kept at the lower end, 220 °C to 230 °C, to reduce odor and volatiles in enclosed chemical areas. End products include dosing skid enclosure panels, acid storage cabinet bodies, brine distribution weir boxes, and chlorine generator housings.
HD0234G40UVL is first extruded into sheet on a single-screw extruder with a sheet die and three-roll stack; the sheet is then reheated and thermoformed on low-pressure forming machines. Because the glass-fiber filler reduces melt sag, the sheet is heated to 190 °C to 210 °C surface temperature using dual-sided quartz or ceramic emitters; forming pressure is 0.6 MPa to 1.0 MPa, and mold temperature is 50 °C to 70 °C. The addition ratio in the extruded sheet remains neat 100% compound to preserve the UV stabilization package; however, trimming scrap up to 10 wt% may be reintroduced into the sheet extrusion feed after dust removal, with the understanding that repeated thermoforming regrind cycles reduce dart impact as measured by ISO 6603-2. Compliance for outdoor enclosures uses ISO 527-2:2012 for tensile strength, ISO 178:2019 for flexural modulus, ISO 4892-2:2013 for weathering, and RoHS Directive 2011/65/EU for restricted substances; when used on public transport interiors, additional smoke-density testing to ISO 5659-2 is performed, but the absence of intrinsic flame retardancy in HDPE may require a separate flame-retardant sheet substrate. End products include recreational vehicle utility access panels, agricultural sprayer belt guards, HVAC condenser louvre shrouds, and material-handling cart side panels.
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The designation HD0234G40UVL within the Aclo Compounders HDPE range identifies a high-density polyethylene matrix modified with a nominal 40% by weight glass-fibre reinforcement and an ultraviolet-stabiliser/lubricant package. The “HD” segment situates the product within the high-density ethylene homopolymer/copolymer class, “0234” denotes the internal base-resin and modifier sequence, “G40” indicates the glass-fibre loading, and “UVL” is conventionally read as UV stabilisation plus processing lubricant. Published lot-specific datasheets for this exact configuration are limited in the public domain; therefore the mechanical envelope below is drawn from analogous 40% glass-fibre HDPE systems and should be confirmed against Aclo Compounders’ certificate of analysis. Candidate service environments include rigid outdoor enclosures, chemically exposed pump components, agricultural guards, and structural brackets where the base HDPE chemical resistance and low-temperature toughness are combined with the stiffness of short-glass reinforcement.
When specimens are injection-moulded according to ISO 294-1 and conditioned at 23 °C and 50% relative humidity, the tensile modulus of a 40% glass-fibre high-density polyethylene compound typically settles between 4,500 MPa and 6,000 MPa. Tensile strength at break under ISO 527-2 is generally reported in the 55 MPa to 75 MPa band, but the elongation at break is sharply reduced relative to unfilled HDPE, commonly falling below 4%. Flexural modulus measured under ISO 178 usually aligns with the tensile modulus trend, occupying a 4,000 MPa to 5,500 MPa range. The notched Charpy impact strength determined under ISO 179-1/1eA is typically 6 kJ/m² to 10 kJ/m² at 23 °C, a value that falls further at sub-zero temperatures because the glass reinforcement limits ductile yielding. Heat deflection temperature under ISO 75-2 method A at 1.8 MPa is expected in the 96 °C to 115 °C window, although flatwise and edgewise orientation of glass fibres produces measurable differences. Melt flow rate determined at 190 °C with 2.16 kg under ISO 1133-1:2022 is typically 2 g/10 min to 8 g/10 min, confirming that the filled system is stiffer in the melt than unfilled HDPE extrusion grades.
| Property | Test method | Typical range | Remarks |
|---|---|---|---|
| Density | ISO 1183-1 | 1.21–1.28 g/cm³ | Glass loading increases density above unfilled HDPE |
| Tensile strength at break | ISO 527-2 | 55–75 MPa | Test speed 5 mm/min |
| Tensile modulus | ISO 527-2 | 4,500–6,000 MPa | Test speed 1 mm/min |
| Flexural modulus | ISO 178 | 4,000–5,500 MPa | Test speed 2 mm/min |
| Notched Charpy impact, 23 °C | ISO 179-1/1eA | 6–10 kJ/m² | Edgewise specimen |
| Heat deflection temperature, 1.8 MPa | ISO 75-2 method A | 96–115 °C | Flatwise; edgewise may differ |
| Melt flow rate, 190 °C/2.16 kg | ISO 1133-1:2022 | 2–8 g/10 min | Dried pellet measurement |
The tensile property scatter is not merely formulation-driven. Glass-fibre length retention during compounding controls stiffness translation; fibre lengths below the critical transfer length reduce modulus even when the nominal glass fraction remains at 40%. Twin-screw compounding with side-fed glass roving after the polymer melt reaches a homogeneous temperature is therefore used to limit fibre attrition. Injection moulding conditions also shift the mechanical response: lower melt temperature and higher injection velocity can preserve longer fibres, but they raise flow-induced orientation and create a wider gap between longitudinal and transverse shrinkage.
Flow-direction shrinkage in glass-reinforced HDPE is consistently lower than transverse-direction shrinkage because fibre orientation aligns with the melt-front advance. For a 40% glass-fibre HDPE compound, flow-direction mould shrinkage is commonly observed in the 0.2% to 0.5% range, while transverse mould shrinkage can reach 0.6% to 1.0% depending on part geometry and gate placement. This anisotropy is a principal design constraint. Flat parts with large uninterrupted flow lengths warp because the high orientation along the flow path restricts contraction, while the transverse direction continues to contract after ejection. Edge-gated rectangular plaques therefore exhibit concave or convex distortion, and the distortion is intensified when one surface cools more slowly than the other.
Tool design for this grade requires a deliberate approach to gate location, wall thickness balancing, and cooling-circuit uniformity. Multiple gates reduce the long flow path, but each weld line created by separate melt fronts becomes a mechanically weakened region. The weld-line strength in 40% glass-filled HDPE can fall to 35% to 55% of the non-weld tensile strength because the fibres do not bridge the weld interface. If a part cannot avoid weld lines, the gate positions should be selected so that weld lines fall in low-stress regions, or the wall section should be locally thickened. Published data for the specific weld-line retention of HD0234G40UVL is limited; candidate moulding trials should quantify the loss under the intended gate scheme.
Drying is not universally mandated for HDPE-based glass-fibre compounds, but storage at relative humidity above 60% can load the glass sizing with moisture. A pre-drying step at 80 °C for 2 h to 4 h using a desiccant dryer is recommended before processing if packaging has been open or if the pellets have been exposed to condensation. Moisture above 0.05% can produce surface splay and reduce fibre-matrix coupling at the interface. During injection moulding, barrel temperatures should be profiled from 190 °C at the feed zone to 220 °C or 230 °C at the nozzle, with melt temperature measured directly rather than inferred from barrel set points. Mould temperatures are commonly held between 20 °C and 60 °C; lower mould temperatures accelerate solidification but also increase frozen-in orientation. Hold pressure should be applied until the gate freezes, and decompression should be minimised because glass-filled melts are less compressible and more prone to screw drool when high decompression is applied.
On a co-rotating twin-screw extruder with an L/D ratio of 40:1, a mid-shear screw configuration with vacuum devolatilisation at approximately -0.08 MPa gauge is appropriate for incorporating the glass reinforcement while limiting polymer degradation. Residence time should not exceed 5 min above 230 °C because HDPE undergoes thermo-oxidative chain scission, and glass-filled HDPE displays the same ceiling as the base polymer. Production-scale experience with filled HDPE shows barrel temperatures above 240 °C produce viscosity loss, discolouration, and an acrid odour from oxidative by-products. The screw should be inspected for abrasive wear when running glass-filled grades; nitrided or bimetallic barrel liners and hardened screw elements are expected for sustained campaigns.
Relative to unfilled HDPE, the 40% glass-fibre compound raises flexural modulus from roughly 1,000 MPa to values in the 4,500–6,000 MPa band, while introducing anisotropic shrinkage and lower unreinforced weld-line efficiency. Tensile strength increases by a factor of approximately 2.5 to 3, but elongation at break collapses from several hundred percent in unfilled HDPE to single-digit values. The glass-reinforced product is therefore unsuitable for snap-fit designs that rely on large post-yield deformation. It is better matched to rigid brackets, housing frames, and support panels where stiffness is the primary requirement and where deflection under load must remain low.
Compared with 30% glass-fibre polypropylene, this HDPE-based compound retains the superior environmental stress-cracking resistance of the ethylene backbone and typically shows lower moisture uptake, but its upper service temperature is lower because the crystalline melting point of HDPE is below that of PP. A 30% glass-fibre PP grade can sustain higher continuous-use temperatures in under-hood applications, whereas the HDPE glass-fibre compound is more attractive in cold environments and in contact with aggressive aqueous chemicals. Against 40% talc-filled HDPE, the glass-fibre product provides higher stiffness and better creep resistance at elevated load, but it also produces greater shrinkage anisotropy and more aggressive wear on screws and moulds. Against 40% glass-fibre polybutylene terephthalate, the HDPE compound is lower in density and better in acid and alkali resistance, but substantially lower in heat deflection temperature and creep resistance above 90 °C.
These differences must be evaluated with specific standardised tests. The replacement of an unfilled HDPE part by the glass-filled grade may require an increase in injection pressure, a reassessment of gate freeze time, and a reduction in flow length because viscosity is higher. Mould-filling analysis should use measured melt-flow data under ISO 1133-1:2022 rather than generic unfilled HDPE rheology. Shrinkage values should be verified on a cavity-pressure-instrumented mould, not on a flat plaque alone, because the pressure history alters packing and therefore anisotropic contraction.
The base olefin matrix can be evaluated under FDA 21 CFR 177.1520 for olefin polymers; however, glass fibre, coupling agents, and UV stabiliser packages require separate migration and end-use suitability review. A final compound intended for repeated food-contact use must be tested under the conditions of use specified in 21 CFR 177.1520, and a letter of no objection or equivalent regulatory confirmation is required before commercial deployment. For outdoor use, the UV-stabiliser package should be assessed under ISO 4892-2 xenon-arc weathering, with colour change and mechanical retention monitored. Glass-filled HDPE exposed to long-wave UV radiation can develop surface chalking if the stabiliser package is depleted; the UVL designation indicates that a stabilised formulation is present, but the specific weathering hours are product-lot dependent. RoHS compliance is typically assessed against Directive 2011/65/EU Annex II substance restrictions, while REACH duties attach to Regulation (EC) No 1907/2006 Annex XVII restrictions and candidate list screening.
| Requirement | Designation | Scope and verification |
|---|---|---|
| RoHS substances | Directive 2011/65/EU Annex II | Pb, Hg, Cd, Cr(VI), PBB, PBDE thresholds |
| REACH | Regulation (EC) No 1907/2006 Annex XVII | Restriction screening and SVHC disclosure |
| Food-contact base resin | FDA 21 CFR 177.1520 | Olefin polymer; final migration testing required |
| Outdoor weathering | ISO 4892-2 | Xenon-arc exposure; mechanical and colour retention |
| Flammability | UL 94 HB | HDPE compounds typically HB at 3.0 mm unless modified |
| Density measurement | ISO 1183-1 | Used for material identification and batch consistency |
Operational boundaries include avoidance of strong oxidising acids above 40 °C, aromatic hydrocarbons, and continuous immersion in chlorinated solvents. The glass-fibre reinforcement does not improve the intrinsic chemical resistance of the HDPE matrix; it only changes the mechanical response. At sub-zero temperatures, the compound retains better impact behaviour than many glass-filled engineering thermoplastics, but the notched impact strength still declines relative to 23 °C values. Parts that must withstand repeated impact at -20 °C should be prototype-tested under ISO 179-1/1eA at the service temperature rather than relying on ambient data. The responsible design review should verify lot-specific melt flow rate, glass content by thermogravimetric analysis, and tensile modulus from each shipment before production release.